IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0572830
(2004-12-16)
|
등록번호 |
US-7422688
(2008-09-09)
|
우선권정보 |
DK-2004 01180(2004-08-03) |
국제출원번호 |
PCT/DK04/000867
(2004-12-16)
|
§371/§102 date |
20070129
(20070129)
|
국제공개번호 |
WO05/026062
(2005-03-24)
|
발명자
/ 주소 |
|
출원인 / 주소 |
|
대리인 / 주소 |
|
인용정보 |
피인용 횟수 :
1 인용 특허 :
4 |
초록
▼
An aerated treatment of water is performed using a serially coupled reactor and flotation tank and is performed using so much activated sludge in the water that small bubbles from an aerator are entrained in the activated sludge, leading some of or all the activated sludge to flotate in the flotatio
An aerated treatment of water is performed using a serially coupled reactor and flotation tank and is performed using so much activated sludge in the water that small bubbles from an aerator are entrained in the activated sludge, leading some of or all the activated sludge to flotate in the flotation tank. A reactor (1) and a flotation tank (36) for performing the process are equipped with at least one aerator (19, 20, 21, 22). A number of preferred processes and designs elaborate on the invention, including how the invention may be incorporated into existing wastewater treatment facilities and exploited there.
대표청구항
▼
The invention claimed is: 1. A process for effecting a continuously or intermittently aerated treatment of water in a loop reactor system, said process comprising the steps of: providing a loop reactor comprising: a propulsive means for driving the circulation of water, sludge, and bubbles through
The invention claimed is: 1. A process for effecting a continuously or intermittently aerated treatment of water in a loop reactor system, said process comprising the steps of: providing a loop reactor comprising: a propulsive means for driving the circulation of water, sludge, and bubbles through a reactor loop; at least one small-bubble aerator capable of producing bubbles small enough to be essentially entrained in said sludge; and means for growing or supplying activated sludge in an amount leading to a concentration of activated sludge in said water in said loop reactor greater than 4 kg of activated sludge per cubic meter of water being treated and high enough to facilitate entrainment of said bubbles from said small-bubble aerator in said sludge; and growing or supplying said activated sludge in an amount leading to a higher concentration of activated sludge in said water in said loop reactor greater than 4 kg of activated sludge per cubic meter of water being treated and high enough to facilitate entrainment of bubbles from said small-bubble aerator, said bubbles thereby becoming essentially entrained in said activated sludge in said water in said loop reactor. 2. The process according to claim 1, wherein said small-bubble aerator is a liquid-liquid ejector being supplied air by introduction of this into its at least one throat, so that the air is being comminuted into said bubbles by the interaction between a motive liquid and a suction liquid inside said ejector. 3. The process according to claim 2 further comprising the step of passing essentially all of said water and its activated sludge through said ejector or a plurality of such ejectors for every loop passage, so that said ejector or plurality of ejectors effectively constitute part of said reactor loop. 4. The process according to claim 3 further comprising the step of generating a driving force provided by said ejector or plurality of ejectors for propelling said water with its sludge and bubbles through said reactor loop. 5. The process according to any of claim 4 further comprising the step of passing said reactor water, for each loop passage, through a centrifugal separator built into said loop reactor for separation of said bubbles from said water. 6. The process according to any of claim 5 further comprising the step of leading said separated bubbles either to the surface of said water or out of said loop reactor. 7. The process according to any of claim 6, wherein said centrifugal separator is a cyclone separator. 8. The process according to claim 6 further comprising the step of introducing air into a peripheral outlet conduit for water and sludge from said centrifugal separator. 9. The process according to any of claim 8 further comprising the step of coupling in series said loop reactor to a flotation tank, and that said small bubbles entrained in said activated sludge inside said loop reactor pass with said water and activated sludge through said conduit to said flotation tank, leading to flotation of some of or all said activated sludge in said flotation tank. 10. The process according to any of claim 9 further comprising the step of supplying less oxygen to said water, for each loop passage, than could have been utilized by said activated sludge in said water during the loop passage. 11. A loop reactor system for effecting a continuously or intermittently aerated treatment of water, said loop reactor system comprising: at least one downcomer and at least one upcomer being interconnected at a lower end of said upcomer and at an upper end of said upcomer, thereby constituting a reactor loop; a propulsive means for driving the circulation of water, sludge, and bubbles through said reactor loop; at least one small-bubble aerator capable of producing bubbles small enough to be essentially entrained in said sludge; means for supplying activated sludge in an amount leading to a concentration of activated sludge in said water in said loop reactor greater than 4 kg of activated sludge per cubic meter of water being treated and high enough to facilitate entrainment of said bubbles from said small-bubble aerator in said sludge; and a centrifugal separator incorporated into the upper part of said upcomer. 12. The loop reactor system according to claim 11, wherein said centrifugal separator is a cyclone separator integrated in such a way into the upper half of said upcomer that essentially all said water passing up through said upcomer passes through said cyclone separator on its way up inside said upcomer. 13. The loop reactor system according to claim 12, wherein said cyclone separator is integrated into the upper quarter of side upcomer. 14. The loop reactor system according to claim 12, wherein said aerator is a liquid-liquid ejector comprising an air inlet aperture positioned adjacent an inlet aperture for an ejector's motive fluid, terminating in a gradually widening outlet section, and constituting an upper connection between said upcomer and said downcomer. 15. The loop reactor system according to claim 14, wherein said ejector further comprises an outlet aperture being completely submerged in said water in said downcomer. 16. The loop reactor system according to claim 11 further comprising a flotation tank having a liquid-liquid ejector being supplied air into it and by the interaction between a motive liquid and a suction liquid committing this air into small bubbles. 17. The loop reactor system according to claim 16 further comprising a conduit leading said water and activated sludge from said loop reactor to said flotation tank. 18. The loop reactor system according to claim 17, wherein said ejector is built into said conduit so that it receives, as a suction fluid to said ejector, the complete flow of water and sludge being led directly into said conduit from said loop reactor. 19. A loop reactor system comprising: a loop reactor comprising: at least one downcomer and at least one upcomer being interconnected at a lower end of said upcomer and at an upper end of said upcomer, thereby constituting a reactor loop; a propulsive means for driving the circulation of water, sludge, and bubbles through said reactor loop; at least one small-bubble aerator capable of producing bubbles small enough to be essentially entrained in said sludge; means for supplying activated sludge in an amount leading to a higher concentration of activated sludge in said water in said loop reactor greater than 4 kg of activated sludge per cubic meter of water being treated and high enough to facilitate entrainment of said bubbles from said small-bubble aerator in said sludge; and a centrifugal separator incorporated into said upper part of said upcomer; a flotation tank having a liquid-liquid ejector being supplied air into it and by the interaction between a motive liquid and a suction liquid committing this air into small bubbles; and a conduit leading said water and activated sludge from said loop reactor to said flotation tank; wherein said ejector is built into said conduit so that it receives, as a suction fluid to said ejector, the complete flow of water and sludge being led directly into said conduit from said loop reactor.
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